RS50662B - NEW SYNTHESIS PROCEDURE AND NEW CRYSTAL FORM OF AGLOMELATIN AS AND PHARMACEUTICAL MIXTURES CONTAINING IT - Google Patents
NEW SYNTHESIS PROCEDURE AND NEW CRYSTAL FORM OF AGLOMELATIN AS AND PHARMACEUTICAL MIXTURES CONTAINING ITInfo
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- RS50662B RS50662B RSP-2008/0552A RSP20080552A RS50662B RS 50662 B RS50662 B RS 50662B RS P20080552 A RSP20080552 A RS P20080552A RS 50662 B RS50662 B RS 50662B
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Abstract
Postupak industrijske sinteze jedinjenja formule (I)naznačen time što sepodvrgava reakciji 7-metoksi-1-tetralon formule (III):sa cijanosirćetnom kiselinom formule (IV):u uslovima eliminacije obrazovane vode, u prisustvu katalitičke količine jedinjenja formule (V):u kojoj R i R', isti ili različiti, svaki predstavlja linearnu ili razgranatu (C3-C10) alkil grupu, nesupstituisanu ili supstituisanu aril grupu, ili nesupstituisanu ili supstituisanu linearnu ili razgranatu (C1-C6) arilalkil grupu,kako bi se dobio, nakon filtracije i ispiranja baznim rastvorom, (7-metoksi-3,4-dihidro-1-naftalenil)acetonitril formule (VI):jedinjenje formule (VI) se podvrgava reakciji sa katalizatorom hidrogenacije u prisustvu alilnog derivata kako bi se dobilo jedinjenje formule (VII):koje se onda podvrgava redukciji sa vodonikom u prisustvu prisustvu Raney-evog nikla u amonijačno etanolnoj sredini, a zatim se prevodi u so pomoću hlorovodonične kiseline kako bi se dobilo jedinjenje formule (VIII):koje se onda podvrgava dejstvu natrijum acetata zatim, sirćetnog anhidrida, kako bi se dobilo jedinjenje formule (I) koje se izoluje u obliku čvrste materije, uz razumevanje da se:- pod arilom podrazumeva fenil, naftil ili bifenil grupa,- izraz "supstituisan" odnosi na formule "arila" i "arilalkila" označavajući da aromatični deo ovih grupa može biti supstituisan sa 1 do 3 iste ili različite grupe, odabrane od linearnog ili razgranatog (C1-C6) alkila, hidroksi i linearnog ili razgranatog (C1-C6) alkoksi,- pod "alilnim derivatom" podrazumeva se potpuni molekul koji sadrži 3 do 10 atoma ugljenika i može imati još 1 do 5 atoma kiseonika i, sadržavati najmanje jedan motiv -CH2-CH=CH2. Prijava sadrži još 18 patentnih zahteva.Process for the industrial synthesis of a compound of formula (I) subjected to reaction of 7-methoxy-1-tetralone of formula (III): with cyanosacetic acid of formula (IV): under conditions of elimination of formed water, in the presence of a catalytic amount of a compound of formula (V): u to which R and R ', the same or different, each represent a linear or branched (C3-C10) alkyl group, unsubstituted or substituted aryl group, or unsubstituted or substituted linear or branched (C1-C6) arylalkyl group, to form, after of filtration and washing with a basic solution, (7-methoxy-3,4-dihydro-1-naphthalenyl) acetonitrile of formula (VI): the compound of formula (VI) is reacted with a hydrogenation catalyst in the presence of an allyl derivative to give the compound of formula (VII) ): which is then subjected to reduction with hydrogen in the presence of the presence of Raney nickel in an ammonia-ethanol environment and then converted to the salt by hydrochloric acid to give the compound of formula (VIII): is then subjected to sodium acetate then acetic anhydride to give the compound of formula (I) which is isolated as a solid, with the understanding that: - aryl means a phenyl, naphthyl or biphenyl group, - the term "substituted" refers to the formulas "aryl" and "arylalkyl" signifying that the aromatic moiety of these groups may be substituted by 1 to 3 of the same or different groups selected from linear or branched (C1-C6) alkyl, hydroxy and linear or branched (C1-C6) alkoxy , - "allyl derivative" means a complete molecule containing 3 to 10 carbon atoms and may have another 1 to 5 oxygen atoms and, containing at least one motive -CH2-CH = CH2. The application contains 18 more claims.
Description
NOVI POSTUPAK SINTEZE I NEW SYNTHESIS PROCEDURE AND
NOVI KRISTALNI OBLIK NEW CRYSTAL SHAPE
AGLOMELATINA KAO I AGGLOMELATIN AS WELL
FARMACEUTSKE SMEŠE KOJE GA PHARMACEUTICAL MIXTURES THAT CONTAIN IT
SADRŽE CONTENTS
Ovaj pronalazak se odnosi na postupak industrijske sinteze agomelatina ili N-[2-(7-metoksi-1-naftil)eti!]acetamida formule (I): This invention relates to the process of industrial synthesis of agomelatine or N-[2-(7-methoxy-1-naphthyl)ethyl]acetamide of formula (I):
Ovaj pronalazak se, isto tako, odnosi na kristalni oblik II agomelatina, postupak njegove proizvodnje, kao i na farmaceutske smeše koje ga sadrže. This invention also relates to the crystalline form II of agomelatine, the method of its production, as well as to pharmaceutical mixtures containing it.
Agomelatin ili W-[2-(7-metoksi-1-naftil)etil]acetamid, poseduje korisna farmakološka svojstva. Agomelatine, or W-[2-(7-methoxy-1-naphthyl)ethyl]acetamide, has beneficial pharmacological properties.
Ispoljava dejstvo dvostruke osobenosti, da je sa jedne strane agonist na receptorima melatoninergičnog sistema, a sa druge strane je antagonist receptora 5-HT2C. Ova svojstva mu daju aktivnost u centralnom nervnom sistemu i, preciznije, u lečenju opšte depresije, sezonskih depresija, poremećaja spavanja, kardiovaskularnih patologija, patologija digestivnog sistema, nesanica i umora kao posledica vremenske razlike, poremećaja apetita i gojaznosti. It exhibits the effect of a double peculiarity, that on the one hand it is an agonist on the receptors of the melatoninergic system, and on the other hand it is an antagonist of the 5-HT2C receptor. These properties give it activity in the central nervous system and, more precisely, in the treatment of general depression, seasonal depression, sleep disorders, cardiovascular pathologies, digestive system pathologies, insomnia and fatigue as a result of time difference, appetite disorders and obesity.
Agomelatin, njegova proizvodnja i njegova upotreba u terapeutske svrhe, opisani su u evropskom patentu EP 0 447 285. Agomelatine, its production and its use for therapeutic purposes are described in European patent EP 0 447 285.
Za procenu farmaceutske koristi od ovog jedinjenja, važno je i da se sa tim može pristupiti u proces izvođenja industrijske sinteze, koji se lako postavlja u industrijski postupak, koji proizvodi agomelatin u dobrom prinosu i odlične čistoće. In order to evaluate the pharmaceutical benefit of this compound, it is also important that it can be used in the process of industrial synthesis, which is easily set up in an industrial process, which produces agomelatine in good yield and excellent purity.
Isto tako je važna mogućnost upotrebe agomelatina u obliku dobro definisane kristalne forme, perfektno reproducibilne i koja ispoljava korisna svojstva u pogledu filtracije i olakšavanja formulisanja. Also important is the possibility of using agomelatine in the form of a well-defined crystalline form, perfectly reproducible and which exhibits useful properties in terms of filtration and formulation facilitation.
PatentEP0 447 285 opisuje pristup od osam etapa do agomelatina, počevši od 7-metoksi-1-tetralona sa prosečnim prinosom ispod 30 %. Patent EP0 447 285 describes an eight-step approach to agomelatine, starting from 7-methoxy-1-tetralone with an average yield below 30%.
Taj postupak predpostavlja dejstvo etil bromoacetata, koje sledi aromatizacija i saponifikacija kako bi se dobila odgovarajuća kiselina, koja se onda transformiše u acetamid, a zatim dehidratise kako bi se dobio (7-metoksi-1-naftil)acetonitril, što sledi redukcija, a onda kondenzacija acetil hlorida. This process involves the action of ethyl bromoacetate, followed by aromatization and saponification to give the corresponding acid, which is then transformed into acetamide, then dehydrated to give (7-methoxy-1-naphthyl)acetonitrile, followed by reduction and then condensation of acetyl chloride.
Preciznije, pristup (7-metoksi-1-naftil)acetonitrilu predpostavlja šest reakcionih etapa i, prebacivanjem na industrijski postupak, brzo su primećene teškoće ovog postupka uglavnom zahvaljujući problemima reproducibilnosti prve etape koja se sastoji od dejstva etil bromoacetata na 7-metoksi-tetralon prema Reformatskv reakciji čime se proizvodi etil (7-metoksi-3,4-dihidro-1(2W)-naftaleniliden)etanoat. More precisely, the approach to (7-methoxy-1-naphthyl)acetonitrile presupposes six reaction stages and, switching to the industrial process, the difficulties of this process were quickly noticed mainly due to the reproducibility problems of the first stage, which consists of the action of ethyl bromoacetate on 7-methoxy-tetralone according to the Reformatsk reaction, which produces ethyl (7-methoxy-3,4-dihydro-1(2W)-naphthalenylidene)ethanoate.
Osim toga, sledeća etapa aromatizacije etil (7-metoksi-3,4-dihidro-1(2H)-nafta!eniliden)etanoata bila je često nepotpuna i proizvodila je, nakon saponifikacije, mešavinu proizvoda koje je teško prečistiti. In addition, the subsequent aromatization step of ethyl (7-methoxy-3,4-dihydro-1(2H)-naphtha!enylidene)ethanoate was often incomplete and produced, after saponification, a product mixture that was difficult to purify.
Literatura opisuje pristup od tri etape do (7-metoksi-1-natfil)acetonitrila, počevši od 7-metoksi-1-tetralona dejstvom LiCH2CN zatim, sledi dehidrogenacija u DDQ (2,3-dihloro-5,6-dicijano-1,4-benzohinon) i, na kraju, dehidratacija u kiseloj sredini (Svnthetic Communication, 2001, 31(4), 621-629). Svaki put je ukupan prinos prosećan (76%) i, pre svega, DDQ koji se koristi u reakciji dehidrogenacije kao i refluks benzena koji je neophodan u trećoj etapi ne odgovaraju Industrijskim uslovima u smislu troškova i prirodne sredine. The literature describes a three-step approach to (7-methoxy-1-natyl)acetonitrile, starting with 7-methoxy-1-tetralone under the action of LiCH2CN, followed by dehydrogenation to DDQ (2,3-dichloro-5,6-dicyano-1,4-benzoquinone) and, finally, dehydration in acidic media (Svnthetic Communication, 2001, 31(4), 621-629). Each time the total yield is average (76%) and, above all, the DDQ used in the dehydrogenation reaction as well as the benzene reflux which is necessary in the third stage do not correspond to Industrial conditions in terms of costs and the natural environment.
Podnosilac danas nudi novi postupak industrijske sinteze kojim se dobija, na reproduktivan način i bez potrebe mukotrpnog prečišćavanja, agomelatin sa čistoćom koja je kompatibilna sa njegovom upotrebom kao aktivnog farmaceutskog principa. The applicant today offers a new process of industrial synthesis which obtains, in a reproducible manner and without the need for painstaking purification, agomelatine with a purity compatible with its use as an active pharmaceutical principle.
Alternativa teškoćama koje se susreću sa postupkom, koji je opisan u patentu EP 0 447 285, postignuta je direktnom kondenzacijom cijano derivata na 7-metoksi-1 -tetralon. An alternative to the difficulties encountered with the process, which is described in patent EP 0 447 285, was achieved by direct condensation of the cyano derivative on 7-methoxy-1-tetralone.
Treba, sem toga da jedinjenje, dobijeno kondenzacijom zatim, bude jednostavno podvrgnuto aromatizaciji kako bi se dobio (7-metoksi-1-naftil)acetonitril bez potrebe za drastičnim uslovima i omogućavajući upotrebu reaktiva kompatibilnih sa zahtevima industrijskog troška i prirodne sredine. It is necessary, besides, that the compound, obtained by condensation, is then simply subjected to aromatization in order to obtain (7-methoxy-1-naphthyl)acetonitrile without the need for drastic conditions and allowing the use of reagents compatible with the requirements of industrial cost and natural environment.
Proizašlo je da (7-metoksi-3,4-dihidro-1-naftalenil)acetonitril predstavlja idealan sintetski intermedijer koji odgovara potrebama zahteva direktne sinteze, koja započinje sa 7-metoksi-1-tetralonom i, daje odličan supstrat za etapu aromatizacije. It turned out that (7-methoxy-3,4-dihydro-1-naphthalenyl)acetonitrile is an ideal synthetic intermediate that meets the needs of direct synthesis, which starts with 7-methoxy-1-tetralone and provides an excellent substrate for the aromatization step.
U literaturi su opisane direktne kondezacije tetralona sa acetonrtrilom ili derivatima acetonitrila. Naročito, patent US 3,992,403 opisuje kondenzaciju cijanometilfosfonata na 6-fluoro-1-tetralon i, patent US 3,931,188 opisuje kondenzaciju acetonitrila na tetralon, koja proizvodi intermedijer cijana, koji direktno ulazi u sledeću reakciju. Direct condensations of tetralone with acetonitrile or acetonitrile derivatives have been described in the literature. In particular, US Patent 3,992,403 describes the condensation of cyanomethylphosphonate on 6-fluoro-1-tetralone and, US Patent 3,931,188 describes the condensation of acetonitrile on tetralone, which produces a cyano intermediate, which directly enters the next reaction.
Primenjeno na 7-metoksi-1-tetralon, kondenzacija acetonitrila proizvodi smešu izomera, glavnog "egzo" i manjinskog "endo", kao prema slici 1: Applied to 7-methoxy-1-tetralone, the condensation of acetonitrile produces a mixture of isomers, the major "exo" and the minor "endo", as per Figure 1:
ta smeša zahteva naknadne uslove drastične aromatizacije, koji nisu kompatibilni sa industrijskim zahtevima u smislu nastavljanja sinteze agomelatina. that mixture requires subsequent conditions of drastic aromatization, which are not compatible with industrial requirements in terms of continuing agomelatine synthesis.
Podnosilac danas nudi novi postupak industrijske sinteze, koji omogućava dobijanje (7-metoksi-1-naftil)acetonitriIa na reproduktivan način i bez potrebe mukotrpnog prečišćavanja, u dve etape samo otpočinjanjem od 7-metoksi-tetraIona, upotrebom kao intermedijera sinteze, (7-metoksi-3,4-dihidro-1-naftalenil)acetonitrila oslobođenog nečistoće "egzo" formule (II): The applicant today offers a new process of industrial synthesis, which allows obtaining (7-methoxy-1-naphthyl)acetonitrile in a reproducible way and without the need for painstaking purification, in two stages only by starting from 7-methoxy-tetraion, using as an intermediate of synthesis, (7-methoxy-3,4-dihydro-1-naphthalenyl)acetonitrile freed from the "exo" impurity of the formula (II):
koji se ne može podvrgnuti reakciji naknadne aromatizacije pod radnim uslovima koji su kompatibilni sa industrijskim zahtevima kako bi se nastavila sinteza agomelatina. which cannot undergo a subsequent aromatization reaction under operating conditions compatible with industrial requirements in order to proceed with the synthesis of agomelatine.
Preciznije, ovaj pronalazak se odnosi na postupak industrijske sinteze jedinjenja formule (I): More precisely, this invention relates to the process of industrial synthesis of compounds of formula (I):
koji se opisuje stavljanjem u reakciju 7-metoksi-1-tetralona formule (III): sa cijanosirćetnom kiselinom formule(IV): u uslovima eliminacije obrazovane vode, u prisustvu katalitičke količine jedinjenja formule (V): u kojoj R iR',isti ili različiti, svaki predstavlja linearnu ili razgranatu (C3-C10) alkil grupu, nesupstituisanu ili supstituisanu aril grupu, ili nesupstituisanu ili supstituisanu linearnu ili razgranatu (Ci-Ce) arilalkil grupu, kako bi se, nakon filtracije i ispiranja baznim rastvorom, dobio (7-metoksi-3,4-dihidro-1-naftalenil)acetonitril formule (VI): jedinjenje formule (VI) se stavlja u reakciju sa katalizatorom hidrogenacije u prisustvu alilnog derivata kako bi se dobilo jedinjenje formule (VII): koje se zatim podvrgava redukciji sa vodonikom u prisustvu Raney-evog nikla u amonijačno etanolnoj sredini, a zatim se prevodi u so pomoću hlorovodonične kiseline kako bi se dobilo jedinjenje formule (VIII): which is described by reacting 7-methoxy-1-tetralone of formula (III): with cyanoacetic acid of formula (IV): under conditions of elimination of formed water, in the presence of a catalytic amount of a compound of formula (V): in which R and R', the same or different, each represent a linear or branched (C3-C10) alkyl group, an unsubstituted or substituted aryl group, or an unsubstituted or substituted linear or branched (Ci-Ce) arylalkyl group, to give, after filtration and washing with base solution, (7-methoxy-3,4-dihydro-1-naphthalenyl)acetonitrile of formula (VI): the compound of formula (VI) is reacted with a hydrogenation catalyst in the presence of an allyl derivative to give the compound of formula (VII): which is then subjected to reduction with hydrogen in the presence of Raney nickel in an ammonia-ethanol medium, and then is translated into salt using hydrochloric acid in order to obtained a compound of formula (VIII):
koje se onda podvrgava dejstvu natrij um acetata zatim, sirćetnog anhidrida, kako bi se dobilo jedinjenje formule (I) koje se izoluje u obliku čvrste materije, which is then subjected to the action of sodium acetate and then acetic anhydride to obtain the compound of formula (I) which is isolated as a solid,
uz razumevanje da se: with the understanding that:
pod arilom podrazumeva fenil, naftil ili bifenil grupa, aryl means a phenyl, naphthyl or biphenyl group,
izraz "supstituisan" odnosi na formule "arila" i "arilalkila" označavajući da aromatični deo ovih grupa može biti supstituisan sa 1 do 3 iste ili različite grupe, odabrane od linearnog ili razgranatog (Ci-Ce) alkila, hidroksi i linearnog ili razgranatog (Ci-Ce) alkoksi, the term "substituted" refers to the formulas "aryl" and "arylalkyl" indicating that the aromatic part of these groups can be substituted with 1 to 3 of the same or different groups, selected from linear or branched (Ci-Ce) alkyl, hydroxy and linear or branched (Ci-Ce) alkoxy,
pod "alilnim derivatom" podrazumeva se potpuni molekul koji sadrži 3 do 10 atoma ugljenika i može imati još 1 do 5 atoma kiseonika i, sadržavati najmanje jedan motiv-CH2-CH=CH2. "allylic derivative" means a complete molecule containing 3 to 10 carbon atoms and may have 1 to 5 more oxygen atoms and, containing at least one motif-CH2-CH=CH2.
Preciznije, u reakciji transformacije jedinjenja formule (III) u jedinjenje formule (VI), obrazovana voda se eliminiše destilacijom. Poželjno, koristi se rastvarač reakcije koji ima temperaturu ključanja višu ili istu kao voda, a još bolje, koji formira azeotrop sa vodom, kao na primer, ksilen, toluen, anizol, etilbenzen, tetrahloroetilen, cikloheksen ili mezitilen. More precisely, in the reaction of the transformation of the compound of formula (III) into the compound of formula (VI), the water formed is eliminated by distillation. Preferably, a reaction solvent is used which has a boiling point higher than or equal to that of water, and even better, which forms an azeotrope with water, such as, for example, xylene, toluene, anisole, ethylbenzene, tetrachloroethylene, cyclohexene, or mesitylene.
Na najbolji način, reakcija transformacije jedinjenja formule (III) u jedinjenje formule (VI) se ostvaruje pod refluksom toluena ili ksilena, a još bolje, pod refluksom toluena. In the best way, the reaction of transformation of the compound of formula (III) into the compound of formula (VI) is carried out under the reflux of toluene or xylene, and even better, under the reflux of toluene.
Povoljno, u reakciji transformacije jedinjenja formule (III) u jedinjenje formule (VI), jedna od grupa R ili R' korišćenog katalizatora, predstavlja linearnu ili razgranatu (C3-C10) alkil grupu, a druga predstavlja grupu arila ili arilalkila. Preciznije, poželjni katalizator je onaj sa formulom (Va): Advantageously, in the reaction of the transformation of the compound of formula (III) into the compound of formula (VI), one of the groups R or R' of the used catalyst represents a linear or branched (C3-C10) alkyl group, and the other represents an aryl or arylalkyl group. More precisely, the preferred catalyst is the one with the formula (Va):
u kojoj R'apredstavlja fenil grupu, koja je nesupstituisana ili supstituisana sa jednom ili više grupa linearnog ili razgranatog (Ci-Cs) alkila, n je 0 ili 1, a R, predstavlja linearnu (C3-C10) alkil grupu. in which R' represents a phenyl group, which is unsubstituted or substituted by one or more linear or branched (Ci-C8) alkyl groups, n is 0 or 1, and R represents a linear (C3-C10) alkyl group.
Veoma povoljno, R'apredstavlja fenil grupu, koja nije supstituisana ili je supstituisana, a preciznije, fenil grupu, koja nije supstituisana. Very advantageously, R' represents an unsubstituted or substituted phenyl group, more specifically an unsubstituted phenyl group.
Grupa Raje, poželjno, heksil grupa. The Raje group is preferably a hexyl group.
Povoljno, n je 1. Advantageously, n is 1.
Katalizator, koji se poželjno upotrebljava u reakciji transformacije jedinjenja formule (III) u jedinjenje formule (VI), a koji je u skladu sa postupkom pronalaska, jeste benzilamonijum heptanoat formule (IX): The catalyst, which is preferably used in the reaction of the transformation of the compound of formula (III) into the compound of formula (VI), and which is in accordance with the process of the invention, is benzylammonium heptanoate of formula (IX):
Povoljno, jedinjenje formule (VI) se dobija nakon filtracije i ispiranja sa organskim baznim rastvorom ili mineralnim, kao: NaOH, KOH, Ca(OH)2, Sr(OH)2ili NH4OH, a još bolje, sa rastvorom natrijum hidroksida. Advantageously, the compound of formula (VI) is obtained after filtration and washing with an organic base solution or mineral, such as: NaOH, KOH, Ca(OH) 2 , Sr(OH) 2 or NH 4 OH, and even better, with sodium hydroxide solution.
Poželjno, reakcija transformacije jedinjenja formule (VI) u jedinjenje formule (VII) se izvodi u refluksu toluena ili ksilena, a još bolje, u refluksu toluena. Preferably, the transformation reaction of the compound of formula (VI) to the compound of formula (VII) is carried out in refluxing toluene or xylene, and even better, in refluxing toluene.
Katalizator, koji se poželjno koristi u reakciji transformacije jedinjenja formule (VI) u jedinjenje formule (VII) jeste katalizator u obliku oksida ili na podlozi, kao na primer, paladijum, platina, nikl, Al203a, preciznije, paladijum. Povoljno, koristiće se paladijum na ugljeniku, preciznije, paladijum na ugljeniku od 1 do 20% i još preciznije, do 5% ili 10%. Poželjno, koristiće se paladijum na ugljeniku u katalitičkim količinama, preciznije, u količinama između 1 do 10% težine katalizatora u odnosu na težinu supstrata, a još najbolje, 5%. The catalyst, which is preferably used in the reaction of the transformation of the compound of formula (VI) into the compound of formula (VII), is a catalyst in the form of an oxide or on a support, such as, for example, palladium, platinum, nickel, Al 2 O 3 a, more precisely, palladium. Advantageously, palladium on carbon will be used, more precisely, palladium on carbon from 1 to 20% and even more precisely, up to 5% or 10%. Preferably, palladium on carbon will be used in catalytic amounts, more specifically, in amounts between 1 to 10% by weight of the catalyst relative to the weight of the substrate, and even better, 5%.
Akceptor vodonika koji se koristi u reakciji transformacije jedinjenja formule (VI) u jedinjenje formule (VII) je, poželjno, alilni derivat a, posebno, alil akrilat ili jedan alilglicidiletar. Alil akrilat, poželjan u postupku koji je u skladu sa pronalaskom jeste alil metakrilat. The hydrogen acceptor used in the transformation reaction of the compound of formula (VI) into the compound of formula (VII) is preferably an allyl derivative and, in particular, an allyl acrylate or an allyl glycidyl ether. The allyl acrylate preferred in the process according to the invention is allyl methacrylate.
Povoljno, reakcija transformacije jedinjenja formule (VII) u jedinjenje formule (VIII), koja je u skladu sa postupkom pronalaska, ostvarena je između 20 i 40°C i, još bolje, između 30 i 40°C, a još bolje, na 40°C. Advantageously, the reaction of transforming the compound of formula (VII) into the compound of formula (VIII), which is in accordance with the process of the invention, is carried out between 20 and 40°C and, more preferably, between 30 and 40°C, and even more preferably, at 40°C.
Na povoljan način, reakcija transformacije jedinjenja formule (VIII) u jedinjenje formule (I) je ostvarena u alkoholnoj sredini i, preciznije, u etanolnoj sredini. Advantageously, the transformation reaction of the compound of formula (VIII) into the compound of formula (I) is carried out in an alcoholic medium and, more precisely, in an ethanolic medium.
Ovaj postupak je posebno koristan iz sledećih razloga: This procedure is particularly useful for the following reasons:
• omogućava dobijanje, industrijskim postupkom, jedinjenja "endo" formule (VI) na isključiv način. Ovaj rezultat je sasvim iznenađujući kada se razmatra literatura koja se odnosi na taj tip reakcije, koji najčešće obezbeđuje dobijanje smeša "egzo" / "endo" (Tetrahedron, 1966, 22, 3021-3026). Ovaj rezultat proizilazi iz upotrebe jedinjenja formule (V), kao katalizatora reakcije, na mestu i umesto amonijum acetata, koji se obično koriste u ovim reakcijama (Buli. Soc. Chim. Fr., 1949, 884-890). • kurs postignute transformacije jedinjenja formule (III) u jedinjenje formule (VI) je veoma visok, nadmoćnih 97 %, naspram onog koji se dobija korišćenjem sirćetne kiseline sa kojom taj kurs ne prelazi 75 %. • korišćenje katalizatora hidrogenacije u prisustvu alilnog derivata i, preciznije, alil metakrilata, za transformaciju jedinjenja formule (VI) u jedinjenje formule (VII) sasvim je kompatibilno sa industrijskim zahtevima cene i prirodne sredine, nasuprot hinonima koji se trenutno koriste. • omogućava, sem toga, dobijanje industrijskim postupkom jedinjenja formule (VII) na isključiv način, naročito oslobođeno proizvoda redukcije koji odgovara formuli (X): • najzad, zapaženo je da su tokovi transformacije jedinjenja formule (VI) u jedinjenje formule (VII) povećani, više od 90%. • enables obtaining, by an industrial process, the "endo" compound of formula (VI) in an exclusive way. This result is quite surprising when considering the literature related to that type of reaction, which most often ensures the obtaining of "exo" / "endo" mixtures (Tetrahedron, 1966, 22, 3021-3026). This result derives from the use of the compound of formula (V) as a reaction catalyst in place of and instead of ammonium acetate, which is usually used in these reactions (Buli. Soc. Chim. Fr., 1949, 884-890). • the rate of achieved transformation of the compound of formula (III) into the compound of formula (VI) is very high, over 97%, compared to the one obtained by using acetic acid, with which the rate does not exceed 75%. • the use of a hydrogenation catalyst in the presence of an allyl derivative and, more precisely, an allyl methacrylate, for the transformation of a compound of formula (VI) into a compound of formula (VII) is quite compatible with industrial cost and environmental requirements, as opposed to quinones currently used. • allows, in addition, to obtain by industrial process the compound of formula (VII) in an exclusive way, especially free of the reduction product corresponding to formula (X): • finally, it was observed that the transformation rates of the compound of formula (VI) into the compound of formula (VII) were increased, more than 90%.
■ opisana je hidrogenacija jedinjenja formule (VII) u prisustvu Ranevevog nikla u amonijačno etanolnoj sredini (J. Med. Chem., 1994, 37(20), 3231-3239) ali su neophodni teški uslovi za prenos na industrijski postupak : reakcija se odvija na 60°C i u toku 15 sati i, konačni prinos je manji od 90%. ■ the hydrogenation of the compound of formula (VII) in the presence of Ranev's nickel in an ammonia-ethanol medium was described (J. Med. Chem., 1994, 37(20), 3231-3239), but difficult conditions are necessary for the transfer to the industrial process: the reaction takes place at 60°C for 15 hours and the final yield is less than 90%.
Ustvari, glavna nepogodnost ove reakcije je istovremeno formiranje "bis" derivata formule (XI): In fact, the main disadvantage of this reaction is the simultaneous formation of "bis" derivatives of formula (XI):
i, poteškoća je savlađivanje toka formiranja ove nečistoće. Procedura ističe od strane zahtevaoca omogućavanje dobijanja jedinjenja formule (VIII) sa jednom količinom nečistoće bis ispod 4%, sa uslovima izvođenja koji su kompatibilni sa industrijskim zahtevima jer se reakcija odvija između 30 i and, the difficulty is mastering the course of formation of this impurity. The procedure pointed out by the applicant enables the preparation of compounds of formula (VIII) with an amount of bis impurity below 4%, with performance conditions compatible with industrial requirements since the reaction takes place between 30 and
40°C kako bi se proizveo prinos veći od 90% i hemijske čistoće veće od 99,5%. • etapa prevođenja u amid se odvija u alkoholnoj sredini, preciznije, etanolnoj, što omogućava veoma lako izolovanje jedinjenja formule (I) sa jednim količinskim prinosom. Ovaj rezultat je potpuno iznenađujući jer je ovaj tip reakcije malo kompatibilan sa rastvaračem za koji se očekuje kompetitivna potrošnja sirćetnog anhidrida. 40°C to produce yields greater than 90% and chemical purity greater than 99.5%. • the stage of conversion to amide takes place in an alcoholic environment, more precisely, ethanolic, which enables very easy isolation of the compound of formula (I) with a single quantitative yield. This result is completely surprising because this type of reaction is hardly compatible with a solvent for which competitive consumption of acetic anhydride is expected.
Jedinjenje formule (VI), koje je dobijeno u skladu sa postupkom pronalaska je novo i korisno je kao intermedijer sinteze agomelatina u kojoj se podvrgava reakciji aromatizacije, koju sledi reakcija redukcije zatim, kuplovanja sa sirćetnim anhidridom. The compound of formula (VI) obtained according to the process of the invention is new and useful as an intermediate in the synthesis of agomelatine in which it undergoes an aromatization reaction, followed by a reduction reaction, then coupling with acetic anhydride.
Pronalazak se, isto tako, odnosi na kristalni II oblik agomelatina dobijen u skladu sa prethodno opisanim postupkom. Konačno, važno je da je moguće dobiti jedan kristalni oblik koji je dobro definisan i savršeno reproducibiian. The invention also relates to the crystalline II form of agomelatine obtained in accordance with the previously described procedure. Finally, it is important that it is possible to obtain a crystal form that is well defined and perfectly reproducible.
Prethodna prijava EP0447285 i Yous et al. (Journal of Medicinal Chemistrv, 1992, 35 (8), 1484-1486) omogućavaju pristup agomelatinu u jednom posebnom kristalnom obliku koji je opisan u Tinant et al. (Acta Cryst., 1994, C50, 907-910). Previous application EP0447285 and Yous et al. (Journal of Medicinal Chemistry, 1992, 35 (8), 1484-1486) provide access to agomelatine in a particular crystalline form described in Tinant et al. (Acta Cryst., 1994, C50, 907-910).
Zahtevalac sada ističe postupak dobijanja agomelatina u jednoj dobro definisanoj kristalnoj formi, savršene reproducibilnosti i koja ispoljava zaista korisne osobine u smislu filtracije i olakšanog formulisanja. The applicant now outlines a process for obtaining agomelatine in a well-defined crystalline form, perfectly reproducible and exhibiting truly useful properties in terms of filtration and ease of formulation.
Preciznije, ovaj pronalazak se odnosi na kristalni II oblik agomelatina, koji se karakteriše sledećim parametrima, koji su dobijeni započinjući od dijagrama praška koji je izveden na difraktometru visoke rezolucije D8 Bruker AXS sa ugaonim područjem 3°-90° na 28, jednog koraka od 0,01° i 30 s po koraku : More specifically, this invention relates to the crystalline form II of agomelatine, which is characterized by the following parameters, which were obtained starting from the powder pattern performed on a high-resolution D8 Bruker AXS diffractometer with an angular range of 3°-90° at 28, one step of 0.01° and 30 s per step:
• kristalno okce monoklinsko, • crystalline okce monoclinic,
• parametri okca : a = 20,0903 A, b = 9, 3194 A, c = 15,4796 A, 8 = 108,667° • loop parameters: a = 20.0903 A, b = 9.3194 A, c = 15.4796 A, 8 = 108.667°
• grupa razmaka : P2,/ r\ • spacing group : P2,/ r\
• broj molekula u okcu : 8 • number of molecules in the cell: 8
• zapremina okca : Vokca= 2746,742 A<3>• volume of the volume: Vokca= 2746.742 A<3>
• gustina : d = 1,13 g/cm<3>. • density: d = 1.13 g/cm<3>.
Dobijanje ovog kristalnog oblika ima za prednost omogućavanje posebno brze i efikasne filtracije, kao i izradu farmaceutskih formulacija koje imaju konstantan i reproducibiian sastav, koje su posebno povoljne kada su ove formulacije namenjene oralnoj primeni. Obtaining this crystalline form has the advantage of enabling particularly fast and efficient filtration, as well as the production of pharmaceutical formulations that have a constant and reproducible composition, which are particularly advantageous when these formulations are intended for oral administration.
Tako dobijeni oblik je dovoljno stabilan da se odobri njegovo produženo lagerovanje bez posebnih uslova temperature, svetla, vlage ili protoka kiseonika. The form thus obtained is stable enough to allow its prolonged storage without special conditions of temperature, light, humidity or oxygen flow.
Farmakološko ispitivanje ovako dobijenog oblika pokazuje važnu aktivnost na centralni nervni sistem, kao i na mikrocirkulaciju, a to omogućava ustanovljavanje njegove upotrebe u lečenju stresa, poremećaja spavanja, strahova, opšte depresije, sezonskih depresija, kardiovaskularnih patologija, patologija digestivnog sistema, nesanica i umora kao posledica vremenske razlike, šizofrenije, napada panike, melanholije, poremećaja apetita, gojaznosti, insomnije, bola, psihotičnih poremećaja, epilepsije, dijabetesa, Parkinsonove bolesti, senilne demencije, različitih zbrka povezanih sa normalnim ili patološkim starenjem, migrene, gubitka pamćenja, Alchajmerove bolesti, kao i za poremećaje cerebralne cirkulacije. U jednom drugom domenu aktivnosti, čini se da se u lečenju, oblik II agomelatina može koristiti kod seksualnih disfunkcija, kako ima svojstva inhibitora ovulacije, imunomodulatora i kako je pogodan da se koristi u tretmanu kancera. Pharmacological examination of the form obtained in this way shows an important activity on the central nervous system, as well as on microcirculation, and this allows establishing its use in the treatment of stress, sleep disorders, fears, general depression, seasonal depression, cardiovascular pathologies, digestive system pathologies, insomnia and fatigue as a result of time difference, schizophrenia, panic attacks, melancholy, appetite disorders, obesity, insomnia, pain, psychotic disorders, epilepsy, diabetes, Parkinson's disease, senile dementia, various disorders associated with normal or pathological aging, migraines, memory loss, Alzheimer's disease, as well as for cerebral circulation disorders. In another domain of activity, it seems that in treatment, form II agomelatine can be used in sexual dysfunctions, as it has the properties of ovulation inhibitor, immunomodulator and as it is suitable to be used in the treatment of cancer.
Kristalni II oblik agomelatina imaće prednost korišćenja u tretmanu opšte depresije, sezonskih depresija, poremećaja spavanja, kardiovaskularnih patologija, patologija digestivnog sistema, nesanica i umora kao posledica vremenske razlike, poremećaja apetita i gojaznosti. The crystalline II form of agomelatine will have the advantage of being used in the treatment of general depression, seasonal depression, sleep disorders, cardiovascular pathologies, digestive system pathologies, insomnia and fatigue as a result of time difference, appetite disorders and obesity.
Pronalazak se, takođe, odnosi na farmaceutske smeše koje sadrže, kao aktivni princip, kristalni II oblik agomelatina sa jednom ili više inertnih podloga, koje nisu otrovne i koje su odgovarajuće. Od farmaceutskih smeša koje su u skladu sa pronalaskom, mogu se posebno navesti one koje su prikladne za primenjivanje: oralno, parenteralno (intravenozno ili sub-kutano), nazalno, jednostavne pilule ili dražeje, granule, sublingvalne pilule, želatinske kapsule, tablete, supozitorije, kremovi, masti, kožni gelovi, injektabilni preparati, suspenzije koje se piju i paste za žvakanje. The invention also relates to pharmaceutical mixtures containing, as an active principle, the crystalline II form of agomelatine with one or more inert bases, which are non-toxic and suitable. Of the pharmaceutical compositions according to the invention, those suitable for administration can be mentioned in particular: oral, parenteral (intravenous or subcutaneous), nasal, simple pills or dragees, granules, sublingual pills, gelatin capsules, tablets, suppositories, creams, ointments, skin gels, injectable preparations, oral suspensions and chewing pastes.
Doziranje koje se koristi je prilagodljivo prema prirodi i ozbiljnosti bolesti, putu primenjivanja, kao i starosti i težini pacijenta. Ovo doziranje varira od 0,1 mg do 1 g dnevno jednom ili više puta. The dosage used is adjustable according to the nature and severity of the disease, the route of administration, as well as the age and weight of the patient. This dosage varies from 0.1 mg to 1 g once or more times a day.
Primerl:/V-[2-(7-metoksi-1 -naftil)etil]acetamldExample: N-[2-(7-methoxy-1-naphthyl)ethyl]acetamide
Korak A : ( 7- metoksl- 3, 4- dihidro- 1- naftalenit) acetonitrllStep A: (7-methoxy-3,4-dihydro-1-naphthalene)acetonitrile
U reaktor od 670 I uneseno je u toluen: 85,0 kg 7-metoksi-1-tetralona, 60,3 kg cijanosirćetne kiseline i 15,6 kg heptanonske kiseline, u prisustvu 12,7 kg benzilamina. Reakciona sredina je dovedena do refluksa. Kad početni supstrat iščezne u potpunosti, rastvor se ohladi i filtrira. Dobijeni talog se ispere toluenom, a zatim se dobijeni filtrat ispere 2N rastvorom sode, onda vodom do neutralne reakcije. Nakon uparavanja rastvarača, dobijena čvrsta masa se rekristališe iz smeše etanol/voda (80/20) kako bi se dobio naslovljeni proizvod u prinosu od 90 % i visoke hemijske čistoće od 99 %. In a 670 I reactor, 85.0 kg of 7-methoxy-1-tetralone, 60.3 kg of cyanoacetic acid and 15.6 kg of heptanoic acid were introduced into toluene, in the presence of 12.7 kg of benzylamine. The reaction medium was brought to reflux. When the initial substrate disappears completely, the solution is cooled and filtered. The obtained precipitate is washed with toluene, and then the obtained filtrate is washed with 2N soda solution, then with water until the reaction is neutral. After evaporation of the solvent, the resulting solid was recrystallized from ethanol/water (80/20) to give the title product in 90% yield and 99% high chemical purity.
Tačka to<p>ljenja: 48- 50°C Melting point: 48-50°C
Korak B:( 7- metoksi- 1- naftil) acetonitrilStep B: (7-methoxy-1-naphthyl)acetonitrile
U reaktor od 670 I uneseno je u toluen 12,6 kg paladijuma na ugljenu od 5% i dovedeno na refluks, zatim je dodato 96,1 kg (7-metoksi-3,4-dihidro-1-naftalenil)acetonitrila u rastvoru u toluenu, kao i 63,7 kg alil metakrilata. Reakcija se nastavlja na refluksu i zatim se podvrgava hromatografiji sa isparljivom fazom. Kad početni supstrat iščezne u potpunosti, reakciona sredina se ohladi na temperaturu sredine i zatim, filtrira. Nakon uparavanja toluena, dobijeni čvrsti ostatak se rekristališe iz smeše etanol/voda (80/20) kako bi se dobio naslovljeni proizvod u prinosu od 91 % i visoke hemijske čistoće od 99 %. 12.6 kg of 5% palladium on carbon was introduced into the 670 I reactor in toluene and brought to reflux, then 96.1 kg of (7-methoxy-3,4-dihydro-1-naphthalenyl)acetonitrile in solution in toluene was added, as well as 63.7 kg of allyl methacrylate. The reaction is continued at reflux and then subjected to volatile phase chromatography. When the initial substrate disappears completely, the reaction medium is cooled to room temperature and then filtered. After evaporation of the toluene, the resulting solid residue was recrystallized from ethanol/water (80/20) to give the title product in 91% yield and 99% high chemical purity.
Tačka topljenja:83°C Melting point: 83°C
Korak C :2-( 7- metoksi- 1- naftil) etanamin, hlorhldratStep C: 2-(7-methoxy-1-naphthyl)ethanamine, hydrochloride
U reaktor od 1100 I uneseno je 80,0 kg jedinjenja dobijenog u koraku B i 24,0 kg Ranevevog nikla u etanolu i 170 I amonijaka. Reakciona sredina je mućkana i podvrgnuta pritisku vodonika od 30 bara, a zatim, dovedena na 40°C. Kada početni supstrat iščezne u potpunosti, rastvarač se upari i dobijeni ostatak se ponovo stavlja u rastvor u etil acetat i doda se 41,5 I 11N rastvora hlorovodonične kiseline. Nakon filtriranja, dobijeni talog se ispere etil acetatom, zatim se osuši u sušnici kako bi se proizveo naslovljeni proizvod sa prinosom od 95,3% i hemijskom čistoćom većom od 99,5%. 80.0 kg of the compound obtained in step B and 24.0 kg of Ranev's nickel in ethanol and 170 L of ammonia were introduced into the 1100 L reactor. The reaction medium was shaken and subjected to a hydrogen pressure of 30 bar, and then brought to 40°C. When the starting substrate has completely disappeared, the solvent is evaporated and the resulting residue is redissolved in ethyl acetate and 41.5 L of 11N hydrochloric acid solution is added. After filtration, the resulting precipitate was washed with ethyl acetate, then dried in an oven to give the title product in 95.3% yield and greater than 99.5% chemical purity.
Tačka topljenja :243°C Melting point: 243°C
Korak_ D_ :N-[ 2-( 7- metoksi- 1- naftil) etil] acetamidStep D: N-[2-(7-methoxy-1-naphthyl)ethyl]acetamide
U reaktor od 1600 I uneseno je 173 kg jedinjenja dobijenog u koraku C i 66 kg natrijum acetata u etanolu. Reakciona sredina je mućkana i zatim je dodato 79 kg sirćetnog anhidrida, reakciona sredina je dovedena na refluks i dodato je 600 I vode. Reakcija je ostavljena da se vrati na t sredine i dobijeni talog se filtrira, ispira smešom etanol/voda 35/65 kako bi se proizveo naslovljeni proizvod sa prinosom od 92,5% i hemijskom čistoćom većom od 99%. 173 kg of the compound obtained in step C and 66 kg of sodium acetate in ethanol were introduced into the 1600 I reactor. The reaction medium was shaken and then 79 kg of acetic anhydride was added, the reaction medium was brought to reflux and 600 L of water was added. The reaction was allowed to return to ambient t and the resulting precipitate was filtered, washed with ethanol/water 35/65 to give the title product in 92.5% yield and greater than 99% chemical purity.
Tačka to<p>ljenja:108°C Melting point: 108°C
Prlmer 2:N-[2-{7-metoksi-1 -naftil)etil]acetamidPrimer 2: N-[2-{7-methoxy-1-naphthyl)ethyl]acetamide
Korak A :( 7- metoksi- 3, 4- dihldro- 1- naftalenH) acetonltrilStep A :( 7- methoxy- 3, 4- dihydro- 1- naphthaleneH) acetonitrile
U reaktor od 670 I uneseno je: 85,0 kg 7-metoksi-1-tetralona, 60,3 kg cijanosirćetne kiseline i 15,6 kg heptanonske kiseline u toluenu, u prisustvu 11,0 kg anilina. Reakciona sredina je dovedena do refluksa. Kada početni supstrat iščezne u potpunosti, rastvor se ohladi i filtrira. Dobijeni talog se ispere toluenom, a zatim se dobijeni filtrat ispere 2N rastvorom sode, onda vodom do neutralne reakcije. Nakon uparavanja rastvarača, dobijena čvrsta masa se rekristališe iz smeše etanol/voda (80/20) kako bi se dobio naslovljeni proizvod u prinosu od 87 % i visoke hemijske čistoće od 99 %. 85.0 kg of 7-methoxy-1-tetralone, 60.3 kg of cyanoacetic acid and 15.6 kg of heptanoic acid in toluene were introduced into the 670 I reactor, in the presence of 11.0 kg of aniline. The reaction medium was brought to reflux. When the initial substrate has completely disappeared, the solution is cooled and filtered. The obtained precipitate is washed with toluene, and then the obtained filtrate is washed with 2N soda solution, then with water until the reaction is neutral. After evaporation of the solvent, the resulting solid was recrystallized from ethanol/water (80/20) to give the title product in 87% yield and 99% high chemical purity.
Tačka topljenja :48- 50°C Melting point: 48- 50°C
Korak B:( 7- metoksi- 1- naftll) acetonitrilStep B: (7-Methoxy-1-naphthyl)acetonitrile
Postupa se kao u koraku B Primera 1. Proceed as in step B of Example 1.
Tačka topljenja :83°C Melting point: 83°C
Korak C :2-( 7- metoksi- 1- naftil) etanamln, hlorhidratStep C: 2-(7-Methoxy-1-Naphthyl)Ethanamlin, Hydrochloride
Postupa se kao u koraku C Primera 1. Proceed as in step C of Example 1.
Tačka topljenja :243°C Melting point: 243°C
Korak D:N- f2-( 7- metoksi- 1- naftil) etinacetamldStep D: N-f2-(7-Methoxy-1-naphthyl)ethynacetamld
Postupa se kao u koraku D Primera 1. Proceed as in step D of Example 1.
Tačka topljenja:108°C Melting point: 108°C
Primar 3:Kristalni II oblik N-[2-(7-metoksi-1-naftil)etil]acetamidaPrimer 3: Crystal form II of N-[2-(7-methoxy-1-naphthyl)ethyl]acetamide
Protokolisanje podataka je izvršeno na difraktometru visoke rezolucije D8 Bruker AXS sa sledećim parametrima : ugaono područje 3°-90° na 28, jedan korak od 0,01° i 30 s po koraku. Prašak /V-[2-(7-metoksi-1-naftil)etil]acetamida, dobijen u Primeru 1, položen je na nosač za postavljanje za prenos. Izvor X zraka je bakama cev (XCuKai= 1,54056 A). Mašina sadrži monohromator unutra (kristal Ge(111)) i čvrsti detektor razlaganja energije (MXP-D1, Moxtec-SEPH). Data recording was performed on a D8 Bruker AXS high-resolution diffractometer with the following parameters: angular range 3°-90° at 28, one step of 0.01° and 30 s per step. The N-[2-(7-methoxy-1-naphthyl)ethyl]acetamide powder obtained in Example 1 was placed on a transfer mount. The X-ray source is a bakama tube (XCuKai= 1.54056 A). The machine contains a monochromator inside (Ge(111) crystal) and a solid energy decomposition detector (MXP-D1, Moxtec-SEPH).
Jedinjenje je odlično kristalisano : širina pruga pri srednjoj visini je reda od 0,07° na 28. The compound is perfectly crystallized: the width of the stripes at medium height is of the order of 0.07° at 28.
Isto tako, određeni su sledeći parametri: Also, the following parameters were determined:
• kristalno okce monoklinsko, • crystalline okce monoclinic,
• parametri okca : a = 20,0903 A, b = 9, 3194 A, c = 15,4796 A, 8 = 108,667° • loop parameters: a = 20.0903 A, b = 9.3194 A, c = 15.4796 A, 8 = 108.667°
• grupa razmaka :P2- j/ n• spacing group :P2- j/ n
• broj molekula u okcu : 8 • number of molecules in the cell: 8
• zapremina okca : Vokca= 2746,742 A<3>• volume of the volume: Vokca= 2746.742 A<3>
• gustina : d = 1,13 g/cm<3>. • density: d = 1.13 g/cm<3>.
Primer 4:Farmaceutska smešaExample 4: Pharmaceutical composition
Formula za izradu 1000 pilula doze od 25 mg : Formula for making 1000 pills of 25 mg dose:
PrimerS:Farmaceutska smešaExample: Pharmaceutical mixture
Formula za izradu 1000 pilula doze od 25 mg : Formula for making 1000 pills of 25 mg dose:
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